CN117965155A - Acidizing, yield increasing and injection increasing agent for oil field - Google Patents

Acidizing, yield increasing and injection increasing agent for oil field Download PDF

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CN117965155A
CN117965155A CN202410371197.3A CN202410371197A CN117965155A CN 117965155 A CN117965155 A CN 117965155A CN 202410371197 A CN202410371197 A CN 202410371197A CN 117965155 A CN117965155 A CN 117965155A
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parts
increasing
acid
agent
injection
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CN117965155B (en
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贾映友
陈玉琨
赖继锋
高兴旺
冯雷
刘凯
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Xinjiang Zhonghai Technology Co ltd
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Abstract

The invention discloses an acidification yield-increasing and injection-increasing agent for an oil field. The composite material consists of the following components in parts by weight: 15-30 parts of organic acid, 5-10 parts of scale remover, 1-3 parts of chelating agent, 3-5 parts of dispersing agent, 3-8 parts of surfactant, 3-6 parts of iron ion stabilizer, 1-3 parts of wetting agent, 3-5 parts of polyacrylamide, 1-3 parts of potassium chloride and 60-150 parts of water. The injection increasing agent can be used in the reservoir acidification construction technology, and can prevent clay minerals from swelling when meeting water, reduce interfacial tension of oil water and inhibit scale. The tartaric acid and chloroacetic acid combination, the hydroxyethylidene ammonium diphosphonate and the maleic acid-acrylic acid copolymer combination, the octylphenol polyoxyethylene ether and the cocamidopropyl hydroxysulfobetaine combination are used for synergistic effect.

Description

Acidizing, yield increasing and injection increasing agent for oil field
Technical Field
The invention belongs to the technical field of oil extraction in an oil field, and particularly relates to an acidification yield-increasing and injection-increasing agent for an oil field.
Background
Acidizing is an effective method for increasing the production of oil wells in sandstone formations. The method is to squeeze acid liquid into stratum through well hole, to erode the communicating pore or natural/hydraulic crack wall rock in reservoir and dissolve the slurry leaking into or lost into stratum pore or crack, to enlarge or dredge stratum seepage channel, improve stratum permeability, and improve stratum diversion capacity, to increase oil well production.
Clay minerals in an oilfield reservoir are adsorbed and injected into water to expand, so that the damage to the reservoir caused by pore permeability of the reservoir is reduced, the water injection pressure of a water injection well is high, and the yield of an oil-gas field is reduced. Corrosion products, scale, bacteria and the like, the injected water can corrode pipelines in the injection process, and the generated corrosion products can cause stratum blockage. The incompatibility of injected water and formation water can produce a large amount of inorganic salt scales which can be adsorbed on the surface of rock to block pore channels.
Disclosure of Invention
The invention aims to provide an acidification yield-increasing injection-increasing agent for an oil field.
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 15-30 parts of organic acid, 5-10 parts of scale remover, 1-3 parts of chelating agent, 3-5 parts of dispersing agent, 3-8 parts of surfactant, 3-6 parts of iron ion stabilizer, 1-3 parts of wetting agent, 3-5 parts of polyacrylamide, 1-3 parts of potassium chloride and 60-150 parts of water.
The organic acid is tartaric acid and chloroacetic acid according to the mass ratio of 3: 1.
The scale remover is prepared from ammonium hydroxyethylidene diphosphonate and maleic acid-acrylic acid copolymer according to the mass ratio of 1: 1.
The chelating agent is one or more of sodium gluconate, ammonium diacetyl amide tetraacetate, sodium nitrilotriacetate and sodium glutamate diacetate.
The dispersing agent is one or more of ethylene glycol butyl ether, ethylene glycol dibutyl ether, coconut oil fatty acid diethanolamide and fatty alcohol polyoxyethylene ether.
The surfactant is octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine according to the mass ratio of 2: 1.
The iron ion stabilizer is one or more of citric acid, fulvic acid, sodium erythorbate and sodium ethylenediamine tetraacetate.
The wetting agent is one or more of sodium methyl siliconate, alkylphenol ethoxylates, cetyltrimethylammonium bromide and oleic acid diethanolamide.
The invention has the beneficial effects that: the injection increasing agent can be used in the reservoir acidification construction technology, and can prevent clay minerals from swelling when meeting water, reduce interfacial tension of oil water and inhibit scale. The tartaric acid and chloroacetic acid combination, the hydroxyethylidene ammonium diphosphonate and the maleic acid-acrylic acid copolymer combination, the octylphenol polyoxyethylene ether and the cocamidopropyl hydroxysulfobetaine combination are used for synergistic effect.
Detailed Description
The present invention will be described more fully hereinafter in order to facilitate an understanding of the present invention. This invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
Example 1
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 22 parts of organic acid, 7 parts of scale remover, 2 parts of ammonium diacetate, 4 parts of ethylene glycol butyl ether, 6 parts of surfactant, 4 parts of citric acid, 2 parts of sodium methyl siliconate, 4 parts of polyacrylamide, 2 parts of potassium chloride and 120 parts of water; the organic acid is tartaric acid and chloroacetic acid according to the mass ratio of 3: 1; the scale remover is prepared from ammonium hydroxyethylidene diphosphonate and maleic acid-acrylic acid copolymer according to the mass ratio of 1: 1; the surfactant is octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine according to the mass ratio of 2: 1.
The acidification yield-increasing and injection-increasing agent for the oil field is prepared according to the following steps: according to the weight portions, 22 portions of organic acid, 7 portions of scale remover, 2 portions of diacetyl amide tetraacetic acid ammonium, 4 portions of glycol butyl ether, 6 portions of surfactant, 4 portions of citric acid, 2 portions of sodium methyl siliconate, 4 portions of polyacrylamide, 2 portions of potassium chloride and 120 portions of water are taken, added into a container, heated to 45 ℃, stirred for 15min and cooled to room temperature (25 ℃), thus obtaining the product.
Example 2
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 18 parts of organic acid, 6 parts of scale remover, 1 part of sodium nitrilotriacetate, 1 part of ethylene glycol dibutyl ether, 2 parts of coconut oil fatty acid diethanolamide, 4 parts of surfactant, 3 parts of fulvic acid, 1 part of alkylphenol ethoxylate, 3 parts of polyacrylamide, 1 part of potassium chloride and 70 parts of water; the organic acid is tartaric acid and chloroacetic acid according to the mass ratio of 3: 1; the scale remover is prepared from ammonium hydroxyethylidene diphosphonate and maleic acid-acrylic acid copolymer according to the mass ratio of 1: 1; the surfactant is octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine according to the mass ratio of 2: 1.
The acidification yield-increasing and injection-increasing agent for the oil field is prepared according to the following steps: 18 parts of organic acid, 6 parts of scale remover, 1 part of sodium nitrilotriacetate, 1 part of ethylene glycol dibutyl ether, 2 parts of coconut fatty acid diethanolamide, 4 parts of surfactant, 3 parts of fulvic acid, 1 part of alkylphenol ethoxylate, 3 parts of polyacrylamide, 1 part of potassium chloride and 70 parts of water are added into a container according to parts by weight, and the mixture is heated to 40 ℃, stirred for 18min and cooled to room temperature (25 ℃), thus obtaining the novel detergent.
Example 3
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 28 parts of organic acid, 9 parts of scale remover, 3 parts of sodium gluconate, 4 parts of fatty alcohol polyoxyethylene ether, 7 parts of surfactant, 3 parts of sodium erythorbate, 3 parts of sodium ethylenediamine tetraacetate, 3 parts of cetyl trimethyl ammonium bromide, 5 parts of polyacrylamide, 3 parts of potassium chloride and 140 parts of water; the organic acid is tartaric acid and chloroacetic acid according to the mass ratio of 3: 1; the scale remover is prepared from ammonium hydroxyethylidene diphosphonate and maleic acid-acrylic acid copolymer according to the mass ratio of 1: 1; the surfactant is octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine according to the mass ratio of 2: 1.
The acidification yield-increasing and injection-increasing agent for the oil field is prepared according to the following steps: 28 parts of organic acid, 9 parts of scale remover, 3 parts of sodium gluconate, 4 parts of fatty alcohol-polyoxyethylene ether, 7 parts of surfactant, 3 parts of sodium erythorbate, 3 parts of sodium ethylenediamine tetraacetate, 3 parts of cetyl trimethyl ammonium bromide, 5 parts of polyacrylamide, 3 parts of potassium chloride and 140 parts of water are added into a container according to parts by weight, heated to 50 ℃, stirred for 12min and cooled to room temperature (25 ℃), so as to prepare the organic acid-containing detergent.
Comparative example 1
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 22 parts of tartaric acid, 7 parts of a scale remover, 2 parts of ammonium diacetamide tetraacetate, 4 parts of ethylene glycol butyl ether, 6 parts of a surfactant, 4 parts of citric acid, 2 parts of sodium methyl siliconate, 4 parts of polyacrylamide, 2 parts of potassium chloride and 120 parts of water; the scale remover is prepared from ammonium hydroxyethylidene diphosphonate and maleic acid-acrylic acid copolymer according to the mass ratio of 1: 1; the surfactant is octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine according to the mass ratio of 2: 1.
The acidification yield-increasing and injection-increasing agent for the oil field is prepared according to the following steps: according to the weight portions, 22 portions of tartaric acid, 7 portions of scale remover, 2 portions of diacetyl amide tetraacetic acid, 4 portions of glycol butyl ether, 6 portions of surfactant, 4 portions of citric acid, 2 portions of sodium methyl siliconate, 4 portions of polyacrylamide, 2 portions of potassium chloride and 120 portions of water are taken, added into a container, heated to 45 ℃, stirred for 15min and cooled to room temperature (25 ℃), thus obtaining the product.
Comparative example 2
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 22 parts of chloroacetic acid, 7 parts of a scale remover, 2 parts of ammonium diacetamide tetraacetate, 4 parts of ethylene glycol butyl ether, 6 parts of a surfactant, 4 parts of citric acid, 2 parts of sodium methyl siliconate, 4 parts of polyacrylamide, 2 parts of potassium chloride and 120 parts of water; the scale remover is prepared from ammonium hydroxyethylidene diphosphonate and maleic acid-acrylic acid copolymer according to the mass ratio of 1: 1; the surfactant is octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine according to the mass ratio of 2: 1.
The acidification yield-increasing and injection-increasing agent for the oil field is prepared according to the following steps: according to the weight portions, 22 portions of chloroacetic acid, 7 portions of scale remover, 2 portions of diacetyl amide tetraacetic acid, 4 portions of ethylene glycol butyl ether, 6 portions of surfactant, 4 portions of citric acid, 2 portions of sodium methyl siliconate, 4 portions of polyacrylamide, 2 portions of potassium chloride and 120 portions of water are taken, added into a container, heated to 45 ℃, stirred for 15min and cooled to room temperature (25 ℃), thus obtaining the product.
Comparative example 3
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 22 parts of organic acid, 7 parts of hydroxyethylidene ammonium biphosphonate, 2 parts of diacetyl amide ammonium tetraacetate, 4 parts of ethylene glycol butyl ether, 6 parts of surfactant, 4 parts of citric acid, 2 parts of sodium methyl silanol, 4 parts of polyacrylamide, 2 parts of potassium chloride and 120 parts of water; the organic acid is tartaric acid and chloroacetic acid according to the mass ratio of 3: 1; the surfactant is octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine according to the mass ratio of 2:1.
The acidification yield-increasing and injection-increasing agent for the oil field is prepared according to the following steps: according to the weight portions, 22 portions of organic acid, 7 portions of hydroxyethylidene ammonium diphosphonate, 2 portions of diacetyl amide tetraacetic acid, 4 portions of ethylene glycol butyl ether, 6 portions of surfactant, 4 portions of citric acid, 2 portions of sodium methyl silanol, 4 portions of polyacrylamide, 2 portions of potassium chloride and 120 portions of water are added into a container, and the mixture is heated to 45 ℃, stirred for 15min and cooled to room temperature (25 ℃), thus obtaining the product.
Comparative example 4
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 22 parts of organic acid, 7 parts of maleic acid-acrylic acid copolymer, 2 parts of ammonium diacetate, 4 parts of ethylene glycol butyl ether, 6 parts of surfactant, 4 parts of citric acid, 2 parts of sodium methyl silanol, 4 parts of polyacrylamide, 2 parts of potassium chloride and 120 parts of water; the organic acid is tartaric acid and chloroacetic acid according to the mass ratio of 3: 1; the surfactant is octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine according to the mass ratio of 2: 1.
The acidification yield-increasing and injection-increasing agent for the oil field is prepared according to the following steps: according to the weight portions, 22 portions of organic acid, 7 portions of maleic acid-acrylic acid copolymer, 2 portions of diacetyl amide tetraacetic acid ammonium, 4 portions of ethylene glycol butyl ether, 6 portions of surfactant, 4 portions of citric acid, 2 portions of sodium methyl silanol, 4 portions of polyacrylamide, 2 portions of potassium chloride and 120 portions of water are added into a container, heated to 45 ℃, stirred for 15min and cooled to room temperature (25 ℃), thus obtaining the product.
Comparative example 5
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 22 parts of organic acid, 7 parts of scale remover, 2 parts of ammonium diacetate, 4 parts of ethylene glycol butyl ether, 6 parts of octyl phenol polyoxyethylene ether, 4 parts of citric acid, 2 parts of sodium methyl siliconate, 4 parts of polyacrylamide, 2 parts of potassium chloride and 120 parts of water; the organic acid is tartaric acid and chloroacetic acid according to the mass ratio of 3: 1; the scale remover is prepared from ammonium hydroxyethylidene diphosphonate and maleic acid-acrylic acid copolymer according to the mass ratio of 1: 1.
The acidification yield-increasing and injection-increasing agent for the oil field is prepared according to the following steps: according to the weight portions, 22 portions of organic acid, 7 portions of scale remover, 2 portions of diacetyl amide tetraacetic acid, 4 portions of ethylene glycol butyl ether, 6 portions of octyl phenol polyoxyethylene ether, 4 portions of citric acid, 2 portions of sodium methyl silanol, 4 portions of polyacrylamide, 2 portions of potassium chloride and 120 portions of water are taken, added into a container, heated to 45 ℃, stirred for 15min and cooled to room temperature (25 ℃), thus obtaining the product.
Comparative example 6
The acidizing, yield increasing and injection increasing agent for the oil field comprises the following components in parts by weight: 22 parts of organic acid, 7 parts of scale remover, 2 parts of ammonium diacetate, 4 parts of ethylene glycol butyl ether, 6 parts of cocamidopropyl hydroxysulfobetaine, 4 parts of citric acid, 2 parts of sodium methyl silanol, 4 parts of polyacrylamide, 2 parts of potassium chloride and 120 parts of water; the organic acid is tartaric acid and chloroacetic acid according to the mass ratio of 3: 1; the scale remover is prepared from ammonium hydroxyethylidene diphosphonate and maleic acid-acrylic acid copolymer according to the mass ratio of 1: 1.
The acidification yield-increasing and injection-increasing agent for the oil field is prepared according to the following steps: according to the weight portions, 22 portions of organic acid, 7 portions of scale remover, 2 portions of ammonium diacetate, 4 portions of glycol butyl ether, 6 portions of cocamidopropyl hydroxysulfobetaine, 4 portions of citric acid, 2 portions of sodium methyl silanol, 4 portions of polyacrylamide, 2 portions of potassium chloride and 120 portions of water are added into a container, heated to 45 ℃, stirred for 15min and cooled to room temperature (25 ℃), thus obtaining the product.
Experimental example:
The anti-swelling performance test is carried out according to the oil industry standard of SY/T5971-94 ' clay stabilizer for Water injection ' performance evaluation method ', wherein the test liquid is 0.5% of the injection enhancer (the injection enhancers prepared in examples 1-3 and comparative examples 1-2), 20% of the composite acid liquid and the balance of water; the raw materials of the composite acid liquor comprise 10% of ammonium fluoride, 20% of hydrochloric acid and the balance of water.
Each group of experiments was averaged 3 times and statistically analyzed using SPSS 24.0 software with the data results measuredThe (mean ± standard deviation) represents that the data normalization test is carried out by adopting a Kolmogorov-Smirnov test method, and the comparison of the mean difference between two groups adopts a t test for data conforming to the normal distribution, and has statistical significance by taking P <0.05 as the difference.
The measurement results are shown in Table 1:
TABLE 1
Note that: * Representing a comparison of P <0.05 with example 1 group.
The expansion resistance of the injection enhancer is an important index, and if the injection enhancer causes the expansion of the clay or rock in the oil layer after injection, the expansion of the clay or rock can cause collapse to prevent further exploitation of petroleum, and as can be seen from table 1, the expansion resistance and the expansion shrinkage of the test solutions of examples 1-3 are equivalent, no significant difference exists, and the expansion resistance and the expansion shrinkage of the test solutions of example 1 are significantly higher than those of comparative examples 1 and 2, so that the combined use of tartaric acid and chloroacetic acid proves to be synergistic.
The interfacial tension was measured using a rotary drop interfacial tension contact angle meter, with a test solution of 0.5% of the injection enhancing agent (the injection enhancing agents prepared in examples 1-3 and comparative examples 5-6), 20% of the composite acid solution, and the balance water; the raw materials of the composite acid liquor comprise 10% of ammonium fluoride, 20% of hydrochloric acid and the balance of water.
The measurement results are shown in Table 2:
TABLE 2
Note that: * Representing a comparison of P <0.05 with example 1 group.
The higher the interfacial tension of the oil layer to be exploited, the more the oil layer is blocked from flowing, and the exploitation efficiency is reduced, as can be seen from table 2, the test liquids of examples 1-3 have comparable interfacial tension without significant difference, and the test liquid of example 1 has significantly lower interfacial tension than comparative examples 5 and 6, which proves the synergistic effect of the combination of octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine.
According to SY/T5673-93 requirements of "method for evaluating performance of anti-fouling agent for oilfield", evaluation experiments are carried out on the performance of the injection-enhancing agent CaCO 3、CaSO4 prepared in examples 1-3 and comparative examples 3-4, the working concentration of the injection-enhancing agent is 0.35%, and the measurement results are shown in Table 3:
TABLE 3 Table 3
Note that: * Representing a comparison of P <0.05 with example 1 group.
The corrosion products, scale matters, bacteria and the like can corrode pipelines in the injection process, and the generated corrosion products can cause formation blockage, so that the scale inhibition performance of the injection enhancing agent is an important performance, and as can be seen from table 3, the scale inhibition rates of the test solutions of examples 1-3 are equivalent, no significant difference exists, the scale inhibition rate of the test solution of example 1 is significantly higher than that of comparative examples 3 and 4, and the combined use of the hydroxyethylethylene diphosphonate and the maleic acid-acrylic acid copolymer proves that the effects are synergistic.
The above examples illustrate only a few embodiments of the invention, which are described in detail and are not to be construed as limiting the scope of the invention. It should be noted that it will be apparent to those skilled in the art that several variations and modifications can be made without departing from the spirit of the invention, which are all within the scope of the invention. Accordingly, the scope of protection of the present invention is to be determined by the appended claims.

Claims (6)

1. The acidizing yield-increasing injection agent for the oil field is characterized by comprising the following components in parts by weight: 15-30 parts of organic acid, 5-10 parts of scale remover, 1-3 parts of chelating agent, 3-5 parts of dispersing agent, 3-8 parts of surfactant, 3-6 parts of ferric ion stabilizer, 1-3 parts of wetting agent, 3-5 parts of polyacrylamide, 1-3 parts of potassium chloride and 60-150 parts of water;
the organic acid is tartaric acid and chloroacetic acid according to the mass ratio of 3: 1; the scale remover is prepared from ammonium hydroxyethylidene diphosphonate and maleic acid-acrylic acid copolymer according to the mass ratio of 1: 1.
2. The acidifying, yield-increasing and injection-increasing agent for oil field according to claim 1, wherein the chelating agent is one or more of sodium gluconate, ammonium diacetamide tetraacetate, sodium nitrilotriacetate and sodium glutamate diacetate.
3. The acidifying agent for increasing yield and injection for oil field of claim 1, wherein the dispersant is one or more of ethylene glycol butyl ether, ethylene glycol dibutyl ether, coconut oil fatty acid diethanolamide, and fatty alcohol polyoxyethylene ether.
4. The acidifying, yield-increasing and injection-increasing agent for oil fields according to claim 1, wherein the surfactant is octyl phenol polyoxyethylene ether and cocamidopropyl hydroxysulfobetaine according to a mass ratio of 2:1.
5. The acidifying agent for increasing yield and injection for oil field of claim 1, wherein the iron ion stabilizer is one or more of citric acid, fulvic acid, sodium erythorbate and sodium ethylenediamine tetraacetate.
6. The acidifying, yield-increasing and injection-increasing agent for oil fields according to claim 1, wherein the wetting agent is one or more of sodium methyl siliconate, alkylphenol ethoxylates, cetyltrimethylammonium bromide and diethanolamide oleate.
CN202410371197.3A 2024-03-29 Acidizing, yield increasing and injection increasing agent for oil field Active CN117965155B (en)

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